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Operating an anaerobic digester for sludge treatment

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Anaerobic digester treating sludge on a wastewater treatment plant

Operating an anaerobic digester

Anaerobic digesters can be operated at different conditions of mixing and temperature. The temperature conditions are normally defined by the types of micro-organisms which are sustained within the temperature range applied, referred to as mesophilic and thermophilic micro-organisms.

Normal parameter value ranges for mesophilic and thermophilic operation for a typical sewage sludge feed are summarised below. Operation outside these ranges (as with low-temperature psychrophilic operation) is possible if the reactor and/or process treatment scheme is appropriately configured or designed.

Table 1. General ranges of key design parameters, sewage sludge
Parameter Meso- Thermo- Notes

VS Volatile solids
OLR Organic loading rate

Temperature, °C30−3949−57Optimal ranges
3555Typical target value
Retention time, d15−305−14
VS reduction, %20−55%20−55%Affected by operating conditions and solids loading & characteristics
OLR, gVS/m3/day0.5−1.61.6−6.5Low end of range for unmixed reactor; high end for mixed

The volatile solids (VS) concentration is taken as equating to the organic, biodegradable fraction of the solids, and the VSS the volatile part of the suspended solids. The organic loading rate (OLR) represents the amount of digestible organic matter per m3 sludge fed into the reactor each day.

A further key operating parameter is the pH. The pH must be kept within a specific optimal range to ensure that the process works effectively, as governed by the biochemical mechanism.

An indication of the range of the characteristics of sludges generated by, or discharged from, the various unit operations in a municipal wastewater treatment scheme can be obtained from reviewing data from a single source, such the Ontario Government’s Design Guidelines For Sewage Works: Sludge Stabilisation, Government of Ontario.

Table 2. Ranges of suggested parameter values for different sewage sludge sources (Adapted from: Design Guidelines For Sewage Works: Sludge Stabilisation, Government of Ontario)
Source Liq. Sludgea Solids concentn. %b − range Solids concentn. %b − average VSSc DS − g/m3,d DS − g/(cap·d)e DS decr. %

DS Dry solids
aLitres of liquid sludge per cubic metre of treated sewage
bTotal solids concentration as percentage of sludge
cPercentage of solids which are volatile
dGrams of dry solids per cubic metre of treated sewage
eGrams of dry solids per inhabitant per day

Primary sedimentation + conventional activated sludge (CAS) + AD
Undigested (no P Removal)4.02–74.56516082
Undigested (w. P Removal)5.02–6.54.060220100
Digested (no P Removal)2.02–65.0501155237%
Digested (w P Removal)3.52–64.0451506832%
Primary sedimentation + AD
Undigested (No P Removal)2.03.5–65.06512055
Undigested (With P Removal)3.23.5–74.56517077
Digested (No P Removal)1.15–86.050753438%
Digested (With P Removal)1.65–86.0501105035%

A key anaerobic digestion operational performance parameter is the amount of methane gas product generated, normally referred to as the methane/gas yield. This is expressed either as the mass of methane per unit mass of volatile solids, or as a percentage.

The other key parameter is the net energy consumption or generation in kWh. This relates to the latent energy of the sludge feed, expressed as the calorific value in kWh per ton of sludge dry solids (DS). In general, the anaerobic digestion process is energy positive: there is more energy provided by the sludge than that required to maintain the AD reactor at the required temperature.

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References

Government of Ontario: Design Guidelines For Sewage Works: Sludge Stabilisation: https://www.ontario.ca/document/design-guidelines-sewage-works/sludge-stabilization#table16-1-note2

About this page

'Operating an anaerobic digester for sludge treatment' was written by Simon Judd

This page was last updated on 19 September 2020

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